14.11.2013 Views

download pdf version of PhD book - Universiteit Utrecht

download pdf version of PhD book - Universiteit Utrecht

download pdf version of PhD book - Universiteit Utrecht

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

7.2 Network Generation<br />

. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .<br />

equations <strong>of</strong> mass balance. Under different saturation states, the flow equations<br />

are first solved and the resulting pore scale velocities are then used to simulate<br />

reactive solute transport.<br />

The main objective <strong>of</strong> this study is a better understanding <strong>of</strong> transport <strong>of</strong><br />

adsorptive/reactive solutes under unsaturated conditions. Although various<br />

mechanisms, such adsorption to the aws common line or moving AW interfaces<br />

have been suggested to affect the adsorptive transport, the exact role <strong>of</strong><br />

these processes are still unclear. In this study, adsorption over a wide range<br />

<strong>of</strong> saturations was considered by taking into account adsorption to both AW<br />

and SW interfaces. Regions <strong>of</strong> the pore space for which a wetting film <strong>of</strong> water<br />

coats the surface remain water-wet, as do the corners <strong>of</strong> the pore space<br />

where water still resides; however, we neglect adsorptive to interfaces associated<br />

with the water films. We have introduced a new formulation <strong>of</strong> adsorptive<br />

solute transport within a pore network which helps to capture the effect <strong>of</strong> limited<br />

mixing and adsorption under partially-saturated conditions. In contrast<br />

to former pore-network studies, which assign one (average) pressure and one<br />

(average) concentration to each pore element, we discretize an individual pore<br />

space into separate smaller domains, each with its own flow rate and solute<br />

concentration, in order to increase the accuracy <strong>of</strong> simulations. Thus, fluid<br />

fluxes along edges <strong>of</strong> each pore are calculated and taken into account in the<br />

simulation <strong>of</strong> adsorptive solute transport.<br />

In this paper, after construction <strong>of</strong> a Multi-Directional Pore-Network (MDPN)<br />

model, quasi-static drainage simulations are performed to determine pore-level<br />

distribution <strong>of</strong> each fluid phase. Then, steady-state flow is established and<br />

equations <strong>of</strong> mass balance for adsorptive solutes are solved to calculate transport<br />

properties <strong>of</strong> such a distribution and to obtain BTCs <strong>of</strong> solute concentration.<br />

Adsorption to both air-water (AW) and solid-water (SW) interfaces is<br />

modeled. These adsorption processes are independent <strong>of</strong> each other and each<br />

<strong>of</strong> them can have its own distribution coefficient and adsorbing area.<br />

7.2 Network Generation<br />

7.2.1 Pore size distributions<br />

In the present study, the pore structure is represented using a 3D MDPN<br />

model. Pore-body radii are assigned from a lognormal distribution, with no<br />

spatial correlation, explained in Section 6.2.<br />

Figure (7.1) shows the bore body size distribution used within the MDPN. Pore<br />

163

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!